CN101584943B - Multi-stage evaporation and air-vapour hybrid system and method thereof - Google Patents
Multi-stage evaporation and air-vapour hybrid system and method thereof Download PDFInfo
- Publication number
- CN101584943B CN101584943B CN200910053929XA CN200910053929A CN101584943B CN 101584943 B CN101584943 B CN 101584943B CN 200910053929X A CN200910053929X A CN 200910053929XA CN 200910053929 A CN200910053929 A CN 200910053929A CN 101584943 B CN101584943 B CN 101584943B
- Authority
- CN
- China
- Prior art keywords
- tower
- liquid
- tower body
- stage evaporation
- vapour
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a multi-stage evaporation and air-vapour hybrid system and method thereof, comprising a multi-stage evaporation tower, a cascade control system for feeding a liquid charging stock, a heater and three nozzles. The multi-stage evaporation tower comprises a tower body and a tower base divided into three segments with two dividing tower plates. The tower body is provided with an air-vapour outlet, a feeding inlet, an air-vapour inlet, a liquid outlet and a leakage fluid drain. The method provided by the invention comprises the following steps: the liquid charging stock is shunted and regulated through the cascade control system, and then fed into an upper tower body of the multi-stage evaporation tower and the heater, and a liquid mixture is heated in the heater. The air is loaded into the nozzle, the liquid mixture is mixed and evaporated in the heater, then air-vapour mixture is fed into the multi-stage evaporation tower. The air-vapour mixture product is discharged from the top and a residual liquid is further discharged. The invention realizes multi-stage evaporation and condensation of the mixture liquid through a plurality of nozzles and multi-stage evaporation tower system, and control is simple.
Description
Technical field
The invention belongs to liquid evaporation and gas-liquid mixed field, particularly a kind of liquid of being made up of a plurality of nozzles and multi-stage evaporation tower evaporates system and the method thereof that gentle vapour mixes.
Background technology
The mixing of liquid evaporation and gas-liquid is widely used in industries such as oil, chemical industry, metallurgy, medicine.Mix at the evaporation of liquid mixture and with gas, the equipment of prior art is introduced gas and vapor mixing after adopting more and repeatedly evaporating in different evaporators again.The defective that adopts this kind mode is that equipment needed thereby quantity is many, and floor space is big, and is complicated to its control.
The method of prior art is: with the liquid evaporation, gas is introduced earlier again.Exist two shortcomings like this, the one, must be heated to it more than boiling temperature during the liquid evaporation, if contain unsaturated compound in the liquid, unsaturated compound can form macromolecular compound by polymerization reaction take place during high temperature, influences subsequent process; The 2nd, evaporated liquid steam and gas are difficult for mixing, and influence both reaction speeds.
Summary of the invention
The system and the method thereof that the object of the present invention is to provide the gentle vapour of a kind of multi-stage evaporation to mix, it has overcome the defective that prior art exists, solved existing problem, finish the repeatedly evaporation and the condensation of mixing material by a plurality of nozzles and multi-stage evaporation tower, promote mixing material fully to evaporate and evenly mix with the gas of input tower body.
Technical solution of the present invention is as follows:
The system that the gentle vapour of a kind of multi-stage evaporation mixes comprises multi-stage evaporation tower, sends into cascade control system, heater and three nozzles of liquid charging stock;
Described multi-stage evaporation tower comprises tower body and the tower seat that is divided into three sections by two disconnected column plates, is equipped with the downspout that is communicated with its upper and lower two sections tower bodies on the described disconnected column plate;
The epimere tower body is provided with gas vapour products export, charging aperture, gas vapor inlet and liquid outlet successively from the top to the bottom; The stage casing tower body is provided with gas vapor outlet, gas vapor inlet and liquid outlet successively from top to the bottom; The hypomere tower body is provided with gas vapor outlet, gas vapor inlet, liquid outlet and leakage fluid dram successively from top to the bottom;
First nozzle connects the gas vapor inlet of gas feed and hypomere tower body, and first nozzle bottom connects heater; Second nozzle connects the gas vapor inlet of stage casing tower body and the gas vapor outlet of hypomere tower body, and second nozzle bottom connects the liquid outlet of stage casing tower body; The 3rd nozzle connects the gas vapor inlet of epimere tower body and the gas vapor outlet of stage casing tower body, and the 3rd nozzle bottom connects the liquid outlet of epimere tower body;
Described cascade control system is by the charging aperture of pipeline connection multi-stage evaporation tower, and cascade control system connects the liquid outlet of heater base and hypomere tower body again by branched pipe.
The present invention takes following further technical measures:
Described cascade control system comprises the control valve of two adjustable throttle amounts that are in series, and two control valves respectively connect the feedstock pump of sending into liquid charging stock and the charging aperture of multi-stage evaporation tower; Be provided with a branched pipe between two control valves, this branched pipe connects the liquid outlet of heater base and hypomere tower body respectively.
Described epimere tower body inside is provided with mist eliminator from gas vapour products export between the charging aperture; Described charging aperture is to being provided with several layers of horizontally disposed tower tray between the gas vapor inlet.
The gas vapour products export on described tower body top and the tower wall between the mist eliminator are provided with thermometer boss and pressure tap.
The gas vapour products export on described tower body top and the tower wall between the thermometer boss are provided with manhole; The tower wall of described tower seat bottom is provided with manhole.
The position of the inherent corresponding charging aperture of described tower body is provided with the charging baffle plate, and this charging baffle plate is a perpendicular type, and its level board face connects the tower wall, and vertical plate is in the face of accurate charging aperture.
The tower wall of described tower seat is provided with leakage fluid dram, is connected with the discharge raffinate by pipeline between leakage fluid dram and the tower body bottom.
A kind of method of implementing the system of the gentle vapour mixing of multi-stage evaporation of the present invention, it may further comprise the steps:
A, send into respectively in multi-stage evaporation tower top tower body and the heater after liquid charging stock regulated by cascade control system shunting;
B, the liquid of partially liq raw material and multi-stage evaporation tower bottom is sent into heater together, liquid mixture is heated in heater;
C, gas is sent into first nozzle, mix the liquid mixture in the evaporation heater and gas vapour mixture is delivered in the hypomere tower body of multi-stage evaporation tower;
D, will enter second nozzle from the gas vapour of hypomere tower body, the liquid of evaporation multi-stage evaporation midsection bottom, the mixture of formation is sent in the multi-stage evaporation midsection;
E, will enter the 3rd nozzle from the gas vapour of stage casing tower body, the liquid of evaporation multi-stage evaporation tower epimere bottom, the mixture of formation is sent in the multi-stage evaporation tower epimere;
F, multi-stage evaporation top of tower are discharged gas vapour mixture finished product, and the liquid bottom will being back to from multi-stage evaporation tower top tower body is sent into the heater heating, and the raffinate that stays is discharged from leakage fluid dram.
Also comprise before the described steps A: the liquid charging stock that prestores enters the various flows value of multi-stage evaporation tower top and heater.
In the described steps A, cascade control system is by the flow of the control valve adjusting two-way liquid charging stock of two adjustable throttle amounts, and control valve is regulated the flow of two-way liquid charging stock according to the flow value that prestores.
The present invention makes it to compare with existing evaporator owing to adopted above technical scheme, has the following advantages and positive effect:
The present invention finishes the repeatedly evaporation and the condensation of mixing material by a plurality of nozzles and multi-stage evaporation Tower System, promotes mixing material fully to evaporate and evenly mixes with the gas of input tower body; Its floor space is little, and control is simple; In multi-stage evaporation tower, owing to have gas, therefore reduced the vapor partial pressure of liquid, can promote that liquid evaporates at a lower temperature; The higher component of gas vapour mid-boiling point in the multi-stage evaporation tower is repeatedly condensed and is become drop, liquid repeatedly with gas vapour mass-and heat-transfer, help the abundant mixing of the gentle vapour of abundant evaporation of liquid.
Description of drawings
Fig. 1 is the schematic diagram of the system of the gentle vapour mixing of a kind of multi-stage evaporation of the present invention.
Fig. 2 is the structural representation of the multi-stage evaporation tower in Fig. 1 system.
Fig. 3 is the method flow diagram that the gentle vapour of a kind of multi-stage evaporation of the present invention mixes.
Drawing reference numeral:
1 is the tower seat, and 2 is manhole, and 3 is downspout, and 4 is interface of the level gauge, 5 is the gas vapor outlet, and 6 is the first disconnected column plate, and 7 is liquid outlet, and 8 is the gas vapor inlet, 9 is the second disconnected column plate, and 10 is tower body, and 11 are the charging baffle plate, 12 is charging aperture, and 13 is thermometer boss, and 14 is gas vapour products export, 15 is manhole, 16 pressure taps, and 17 is mist eliminator, 18 is tower tray, and 19 is the gas vapor inlet, and 20 is liquid outlet, 21 is the gas vapor outlet, and 22 is downspout, and 23 is the gas vapor inlet, 24 is liquid outlet, and 25 is leakage fluid dram, and 30 is multi-stage evaporation tower, 31 is first nozzle, and 32 is second nozzle, and 33 is the 3rd nozzle, 34 is heater, and 35 is feedstock pump, and 36 is cascade control system.
The specific embodiment
Specifically introduce a preferred embodiment of the system of the gentle vapour mixing of multi-stage evaporation of the present invention below in conjunction with accompanying drawing 1～3.
Referring to Fig. 1, the system that the gentle vapour of a kind of multi-stage evaporation of the present invention mixes is made up of multi-stage evaporation tower 30, the cascade control system 36 of sending into liquid charging stock, heater 34 and three nozzles 31,32,33.
Referring to Fig. 2, multi-stage evaporation tower 30 is made up of tower seat 1 and tower body 10.Tower body 10 is one and is divided into three sections tower body 10 by two blocks of disconnected column plates 6,9, on the disconnected column plate 6,9 downspout 3,22 that is communicated with its two sections tower bodies in upper and lower is set all.By being welded to connect, all liq evaporation and gas-liquid blend step all carry out in tower body 10 between tower seat 1 and the tower body 10.
Tower body inside connects disconnected column plate 6,9, tower tray 18 and mist eliminator 17 by bolt.Charging baffle plate 11 and tower body 10 are by being welded to connect.Between at the bottom of the first disconnected column plate 6 and the tower is the hypomere of multi-stage evaporation tower 30, is the stage casing of multi-stage evaporation tower 30 between the first disconnected column plate 6 and the second disconnected column plate 9, is the epimere of multi-stage evaporation tower 30 between the second disconnected column plate 9 and the cat head.
The tower wall of hypomere tower body is provided with gas vapor inlet 23 gentle vapor outlets 5, and gas vapor inlet 23 gentle vapor outlets 5 are along the axle center symmetric arrangement of tower body 10, and are highly different.The bottom of hypomere tower body is provided with a liquid outlet 24, and liquid enters in other vaporising device such as the heater 34 by liquid outlet 24.The first disconnected column plate 6 is provided with downspout 3, and downspout 3 is communicated with hypomere tower body and stage casing tower body.In the hypomere tower body, on Qi Tabi, be provided with the interface of the level gauge 4 of two differing heights, so that liquid level gauge to be installed, be used to measure the liquid level of hypomere tower body bottom.These two interface of the level gauge 4 all are lower than the gas vapor inlet 23 gentle vapor outlets 5 in this section tower body 10.On the tower wall of tower seat 1, be provided with leakage fluid dram 25, be connected by steel pipe between leakage fluid dram 25 and tower body 10 bottoms, derive the liquid that converges at the bottom of the tower.
The tower wall of stage casing tower body is provided with gas vapor inlet 8 gentle vapor outlets 21, and gas vapor inlet 8 gentle vapor outlets 21 are along the axle center symmetric arrangement of tower body 10, and are highly different.The top edge of the first disconnected column plate 6 is provided with a liquid outlet 7, and liquid enters other vaporising device as in second nozzle 32 by liquid outlet 7.The second disconnected column plate 9 is provided with downspout 22, and downspout 22 is communicated with stage casing tower body and epimere tower body.
The tower wall of epimere tower body is provided with charging aperture 12, and the position of tower body 10 inherent corresponding charging apertures 12 is provided with charging baffle plate 11, and this charging baffle plate 11 is a perpendicular type, and charging is flow on the tower tray 18 on request, and its level board face connects the tower wall, and vertical plate is in the face of accurate charging aperture 12.Along horizontal plane ten layers of non-partition-type tower tray 18 are installed in the tower body 10 below charging aperture 12,1#～10# has represented one to ten layer of non-partition-type tower tray 18 among the figure.On the tower wall of tower body 10 below ten layers of tower tray 18, be provided with gas vapor inlet 19.Mist eliminator 17 is set above charging aperture 12.Gas vapour products export 14 is set on the top of tower body 10.Between the tower wall of the edge of tower tray 18 and tower body 10, all leave gas vapour passage.Face the axle center symmetric arrangement of the gas vapour passage of two-layer tower tray 18 along tower body 10 mutually, tower tray 18 has increased the surface area that liquid mixes with gas vapour and the length of mixture length, and liquid is fully mixed with gas vapour.The top edge of the second disconnected column plate 9 is provided with a liquid outlet 20, and liquid enters other vaporising device as in the 3rd nozzle 33 by liquid outlet 20.According to differing heights manhole 15, thermometer boss 13 and pressure tap 16 are set respectively on the tower wall of tower body 10 from gas vapour products export 14 to mist eliminator 17.Thermometer boss 13 connects thermometer, and pressure tap 16 connects pressure gauge, can be to temperature and the pressure data in the outside sends multi-stage evaporation tower epimere tower body, with the temperature and pressure of control tower.
On the tower wall of tower seat 1 bottom manhole 2 is set, the maintenance personal can enter in the tower body 10 by the manhole 15 and the manhole 2 of diverse location, carries out the maintenance repair operation.
Referring to Fig. 1, gas vapor inlet 23, the first nozzles 31 bottoms that first nozzle 31 connects gas feed and hypomere tower body connect heater 34 again.The gas vapor inlet 8 of second nozzle, 32 connection stage casing tower bodies and gas vapor outlet 5, the second nozzles 32 bottoms of hypomere tower body connect the liquid outlet 7 of stage casing tower body.The gas vapor inlet 19 of the 3rd nozzle 33 connection epimere tower bodies and gas vapor outlet 21, the three nozzles 33 bottoms of stage casing tower body connect the liquid outlet 20 of epimere tower body.
Referring to Fig. 3, by the method that the gentle vapour of a kind of multi-stage evaporation of the present invention mixes, the system that adopts the gentle vapour of above-mentioned multi-stage evaporation to mix, this method may further comprise the steps:
1, the liquid charging stock that prestores enters the various flows value of multi-stage evaporation tower 30 tops and heater 34.
2, after being regulated by cascade control system 36 shunting, liquid charging stock sends into respectively in multi-stage evaporation tower 30 top tower bodies and the heater 34.Cascade control system 36 is by the flow of the control valve adjusting two-way liquid charging stock of two adjustable throttle amounts, and control valve is regulated the flow of two-way liquid charging stock according to the flow value that prestores.
3, the liquid of partially liq raw material and multi-stage evaporation tower 30 bottoms is sent into heater 34 together, add liquid mixture in the hot heater 34 by thermal material.
4, gas is sent into first nozzle 31, the liquid mixture that mixes in the evaporation heater 34 is also delivered to gas vapour mixture in the hypomere tower body of multi-stage evaporation tower 30.
5, will enter second nozzle 32 from the gas vapour of hypomere tower body, the liquid of bottom, evaporation multi-stage evaporation tower 30 stage casings, the mixture of formation is sent in multi-stage evaporation tower 30 stage casings.
6, will enter the 3rd nozzle 33 from the gas vapour of stage casing tower body, the liquid of evaporation multi-stage evaporation tower 30 epimeres bottom, the mixture of formation is sent in multi-stage evaporation tower 30 epimeres.
7, gas vapour mixture finished product is discharged at multi-stage evaporation tower 30 tops, and the liquid bottom will being back to from multi-stage evaporation tower 30 top tower bodies is sent into heater 34 heating, and the raffinate that stays is discharged from leakage fluid dram 25.
In conjunction with referring to Fig. 1 and Fig. 2, liquid charging stock is sent in multi-stage evaporation tower 30 tops and the heater 34 by feedstock pump 35 pressurizations, and according to set point adjustment, the raw material that enters from multi-stage evaporation tower 30 tops plays the effect of backflow to both flows by cascade control system 36.Another part raw material and multi-stage evaporation tower 30 bottom liquids are admitted to heater 34 together, and liquid mixture is heated in heater 34.
Gas enters first nozzle 31, in first nozzle 31, form low-pressure area and reduce the liquid vapour dividing potential drop, thereby form evaporation power, this evaporation power makes the liquid mixture evaporation that reaches uniform temperature in the heater 34, and gas vapour mixture is delivered in the multi-stage evaporation tower 30 hypomere tower bodies.After the gas vapour that contains raw material enters the hypomere of multi-stage evaporation tower from gas vapor inlet 23, because flow velocity reduces, increased pressure, the higher component of boiling point forms drop and comes together at the bottom of the tower, the gas vapour that separates the higher drop of boiling point enters other vaporising device as in second nozzle 32 by gas vapor outlet 5, the liquid that converges at the bottom of the tower enters in other vaporising device such as the heater 34 by liquid outlet 24, is difficult to evaporated liquid and discharges from leakage fluid dram 25.
Gas vapour from the hypomere tower body forms low-pressure area and reduces the liquid vapour dividing potential drop in second nozzle 32, thereby forms evaporation power, and this evaporation power makes the liquid evaporation of multi-stage evaporation midsection bottom, and the mixture of formation is sent in the multi-stage evaporation midsection.Because flow velocity reduces, increased pressure, the higher component of boiling point forms drop and comes together on the first disconnected column plate 6, the gas vapour that separates the higher drop of boiling point enters other vaporising device as in the 3rd nozzle 33 by gas vapor outlet 21, the liquid that converges to the first disconnected column plate 6 enters other vaporising device as in second nozzle 32 by liquid outlet 7, and excess liquid enters the hypomere tower body from downspout 3.
Gas vapour from the stage casing tower body forms low-pressure area and reduces the liquid vapour dividing potential drop in the 3rd nozzle 33, thereby forms evaporation power, and this evaporation power makes the liquid evaporation of multi-stage evaporation tower epimere bottom, and the mixture of formation is sent in the multi-stage evaporation tower epimere.Because flow velocity reduces, increased pressure, the higher component of boiling point forms drop and comes together on the second disconnected column plate 9, the gas vapour that separates the higher drop of the boiling point raw material liq that descends that moves upward and reflux carries out mass-and heat-transfer on tower tray 18, its heavy ends condense into downward liquid flow and converge on the second disconnected column plate 9, gas vapour continues to move upward, under in mist eliminator 17, drop being captured, the gas vapour that does not contain liquid enters next procedure from 14 discharges of gas vapour products export, the liquid that converges on the second disconnected column plate 9 enters other vaporising device as in the 3rd nozzle 33 by liquid outlet 20, and excess liquid enters the stage casing tower body from downspout 22.
Meet the requirements of gas vapour mixture and be sent to next procedure from the multi-stage evaporation top of tower, the liquid bottom will being back to from multi-stage evaporation tower 30 top tower bodies is sent into heater 34, and the high-temp liquid that will be difficult to evaporate is discharged from the leakage fluid dram 25 of multi-stage evaporation tower bottom simultaneously.
In summary, the present invention finishes the repeatedly evaporation and the condensation of mixing material by a plurality of nozzles and multi-stage evaporation Tower System, promotes mixing material fully to evaporate and evenly mixes with the gas of input tower body; Its floor space is little, and control is simple; In multi-stage evaporation tower, owing to have gas, therefore reduced the vapor partial pressure of liquid, can promote that liquid evaporates at a lower temperature; The higher component of gas vapour mid-boiling point in the multi-stage evaporation tower is repeatedly condensed and is become drop, liquid repeatedly with gas vapour mass-and heat-transfer, help the abundant mixing of the gentle vapour of abundant evaporation of liquid.
Certainly, those skilled in the art in the present technique field will be appreciated that, the foregoing description only is to be used for illustrating the present invention, and be not as limitation of the invention, as long as in connotation scope of the present invention, all will drop in the scope of claim of the present invention conversion, the modification of the foregoing description.
Claims (10)
1. the system mixed of the gentle vapour of a multi-stage evaporation comprises multi-stage evaporation tower, sends into cascade control system, heater and three nozzles of liquid charging stock, it is characterized in that:
Described multi-stage evaporation tower comprises tower body and the tower seat that is divided into three sections by two disconnected column plates, is equipped with the downspout that is communicated with its upper and lower two sections tower bodies on the described disconnected column plate;
The epimere tower body is provided with gas vapour products export, charging aperture, gas vapor inlet and liquid outlet successively from the top to the bottom; The stage casing tower body is provided with gas vapor outlet, gas vapor inlet and liquid outlet successively from top to the bottom; The hypomere tower body is provided with gas vapor outlet, gas vapor inlet, liquid outlet and leakage fluid dram successively from top to the bottom;
First nozzle connects the gas vapor inlet of gas feed and hypomere tower body, and first nozzle bottom connects heater; Second nozzle connects the gas vapor inlet of stage casing tower body and the gas vapor outlet of hypomere tower body, and second nozzle bottom connects the liquid outlet of stage casing tower body; The 3rd nozzle connects the gas vapor inlet of epimere tower body and the gas vapor outlet of stage casing tower body, and the 3rd nozzle bottom connects the liquid outlet of epimere tower body;
Described cascade control system is by the charging aperture of pipeline connection multi-stage evaporation tower, and cascade control system connects the liquid outlet of heater base and hypomere tower body again by branched pipe.
2. the system that the gentle vapour of multi-stage evaporation according to claim 1 mixes, it is characterized in that: described cascade control system comprises the control valve of two adjustable throttle amounts that are in series, and two control valves respectively connect the feedstock pump of sending into liquid charging stock and the charging aperture of multi-stage evaporation tower; Be provided with a branched pipe between two control valves, this branched pipe connects the liquid outlet of heater base and hypomere tower body respectively.
3. the system that the gentle vapour of multi-stage evaporation according to claim 1 mixes, it is characterized in that: described epimere tower body inside is provided with mist eliminator from gas vapour products export between the charging aperture; Described charging aperture is to being provided with several layers of horizontally disposed tower tray between the gas vapor inlet.
4. the system that the gentle vapour of multi-stage evaporation according to claim 3 mixes, it is characterized in that: the gas vapour products export on described tower body top and the tower wall between the mist eliminator are provided with thermometer boss and pressure tap.
5. the system that the gentle vapour of multi-stage evaporation according to claim 4 mixes, it is characterized in that: the gas vapour products export on described tower body top and the tower wall between the thermometer boss are provided with manhole; The tower wall of described tower seat bottom is provided with manhole.
6. the system that the gentle vapour of multi-stage evaporation according to claim 1 mixes is characterized in that: the position of the inherent corresponding charging aperture of described tower body is provided with the charging baffle plate, and this charging baffle plate is a perpendicular type, and its level board face connects the tower wall, and vertical plate is in the face of accurate charging aperture.
7. the system that the gentle vapour of multi-stage evaporation according to claim 1 mixes, it is characterized in that: the tower wall of described tower seat is provided with leakage fluid dram, is connected with the discharge raffinate by pipeline between leakage fluid dram and the tower body bottom.
8. method of implementing the system that the gentle vapour of the described multi-stage evaporation of claim 1 mixes is characterized in that it may further comprise the steps:
A, send into respectively in multi-stage evaporation tower top tower body and the heater after liquid charging stock regulated by cascade control system shunting;
B, the liquid of partially liq raw material and multi-stage evaporation tower bottom is sent into heater together, liquid mixture is heated in heater;
C, gas is sent into first nozzle, mix the liquid mixture in the evaporation heater and gas vapour mixture is delivered in the hypomere tower body of multi-stage evaporation tower;
D, will enter second nozzle from the gas vapour of hypomere tower body, the liquid of evaporation multi-stage evaporation midsection bottom, the mixture of formation is sent in the multi-stage evaporation midsection;
E, will enter the 3rd nozzle from the gas vapour of stage casing tower body, the liquid of evaporation multi-stage evaporation tower epimere bottom, the mixture of formation is sent in the multi-stage evaporation tower epimere;
F, multi-stage evaporation top of tower are discharged gas vapour mixture finished product, and the liquid bottom will being back to from multi-stage evaporation tower top tower body is sent into the heater heating, and the raffinate that stays is discharged from leakage fluid dram.
9. method according to claim 8 is characterized in that, also comprise before the described steps A: the liquid charging stock that prestores enters the various flows value of multi-stage evaporation tower top and heater.
10. method according to claim 9 is characterized in that, in the described steps A, cascade control system is by the flow of the control valve adjusting two-way liquid charging stock of two adjustable throttle amounts, and control valve is regulated the flow of two-way liquid charging stock according to the flow value that prestores.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910053929XA CN101584943B (en) | 2009-06-26 | 2009-06-26 | Multi-stage evaporation and air-vapour hybrid system and method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910053929XA CN101584943B (en) | 2009-06-26 | 2009-06-26 | Multi-stage evaporation and air-vapour hybrid system and method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101584943A CN101584943A (en) | 2009-11-25 |
| CN101584943B true CN101584943B (en) | 2010-12-01 |
Family
ID=41369496
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910053929XA Expired - Fee Related CN101584943B (en) | 2009-06-26 | 2009-06-26 | Multi-stage evaporation and air-vapour hybrid system and method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101584943B (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101890316B (en) * | 2010-07-08 | 2012-07-11 | 宝钢工程技术集团有限公司 | Method for evaporating liquid and mixing gas and steam |
| CN102371077B (en) * | 2010-08-17 | 2013-11-20 | 珠海市洁星洗涤科技有限公司 | Evaporating tower providing rapidly acquired evaporation capacity |
| CN102600627B (en) * | 2011-12-23 | 2014-03-12 | 安徽国孚润滑油工业有限公司 | Cyclone-flash cloth-film-reboiling-type heat-pipe distiller |
| CN104147800B (en) * | 2014-08-27 | 2017-01-18 | 江苏凯茂石化科技有限公司 | Two-stage methanol evaporation column and methanol evaporation technology method |
| CN107188258B (en) * | 2017-07-20 | 2023-07-14 | 中国华电科工集团有限公司 | Evaporation device applied to desulfurization wastewater and control method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6086055A (en) * | 1998-10-05 | 2000-07-11 | Air Products And Chemicals, Inc. | Combined vapor/liquid distributor for packed columns |
| CN2785674Y (en) * | 2005-04-25 | 2006-06-07 | 余家骧 | Raw material liquid evaporation device possessing liquid distributor mounted in fluid bed |
| CN101240957A (en) * | 2007-10-16 | 2008-08-13 | 何淦明 | Superposition type multilevel evaporation core body |
-
2009
- 2009-06-26 CN CN200910053929XA patent/CN101584943B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6086055A (en) * | 1998-10-05 | 2000-07-11 | Air Products And Chemicals, Inc. | Combined vapor/liquid distributor for packed columns |
| CN2785674Y (en) * | 2005-04-25 | 2006-06-07 | 余家骧 | Raw material liquid evaporation device possessing liquid distributor mounted in fluid bed |
| CN101240957A (en) * | 2007-10-16 | 2008-08-13 | 何淦明 | Superposition type multilevel evaporation core body |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101584943A (en) | 2009-11-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101584943B (en) | Multi-stage evaporation and air-vapour hybrid system and method thereof | |
| EP3247486B1 (en) | Heat exchange and/or mass transfer column comprising a gas distributor and method for distributing gas | |
| US20120125761A1 (en) | Heat integrated distillation apparatus | |
| US9908060B2 (en) | Heat integrated distillation apparatus | |
| US9278295B2 (en) | Heat integrated distillation apparatus | |
| US9266034B2 (en) | Heat integrated distillation apparatus | |
| KR101792347B1 (en) | Distillation device | |
| CN101323553A (en) | Method for increasing temperature of ethylene unit quenching oil tower bottom | |
| WO2012055145A1 (en) | Distillation tower for improving yield of petroleum hydrocarbon distillate and feeding method thereof | |
| CN114432726B (en) | Thermal coupling rectifying tower | |
| RU2544994C1 (en) | Method and unit for oil preliminary distillation | |
| CN103788993B (en) | A kind of catalytic cracking unit | |
| CN102985146B (en) | Method and apparatus for distilling temperature sensitive liquids | |
| CN201426988Y (en) | Multi-section evaporation tower | |
| CN103182194A (en) | Integrated-type liquid vaporization-separation tank device | |
| RU2290244C1 (en) | Method of separation of the liquid components mixture | |
| CN103706139A (en) | Nitrobenzene vaporization distillation mixer | |
| CN102626555B (en) | Acetic acid evaporation and gas mixing integrated device | |
| CN102559247B (en) | The crude oil atmospheric vacuum distillation method of multi-stage vaporizing and device | |
| RU2493897C1 (en) | Method of gas condensate and light oil separation and plant to this end | |
| CN205252718U (en) | Vertical gas -liquid separator | |
| CN212187841U (en) | C9 arene and C8 arene separating device | |
| CN212119963U (en) | Continuous esterification fractionating equipment for synthesizing butyl oleate and butyl palmitate | |
| CN104449826B (en) | A kind of method that reduces ethylene unit quench oil viscosity | |
| CN203187630U (en) | Raw material distribution valve of delayed coking coke tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: BAOSTEEL ENGINEERING + TECHNOLOGY GROUP CO., LTD. Free format text: FORMER OWNER: SHANGHAI BAOSTEEL ENGINEERING + TECHNOLOGY CO., LTD Effective date: 20100701 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20100701 Address after: 201900 Shanghai city Baoshan District Tieli Road No. 2510 Applicant after: Baosteel Engeneering &Technology Group Co., Ltd. Address before: 201900 Shanghai city Baoshan District Tieli Road No. 2510 Applicant before: Shanghai Baogang Engineering Technology Co., Ltd. |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shahe Longcheng Fine Chemical Co., Ltd. Assignor: Baosteel Engeneering &Technology Group Co., Ltd. Contract record no.: 2011310000192 Denomination of invention: Multi-stage evaporation and air-vapour hybrid system and method thereof Granted publication date: 20101201 License type: Exclusive License Open date: 20091125 Record date: 20110907 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101201 Termination date: 20150626 |
|
| EXPY | Termination of patent right or utility model |